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451320177GuangzhouChemicalIndustryVol.45No.13Jul.2017112121212114500012450001。UASB、EGSB、IC、、。。X703.3A1001-9677201713-0032-03ResearchProgressonHigh-rateAnaerobicReactorYANGShan1MAXiao-jian12CHENJun-ying12FANGShu-qi12BAIJing12CAILi-fang11SchoolofChemicalEngineeringandEnergyZhengzhouUniversityHenanZhengzhou4500012EngineeringLaboratoryofHenanProvinceforBio.RefineryTechnologyandEquipmentHenanZhengzhou450001ChinaAbstractForsolvingtheincreasinglyseriousenvironmentalandenergyissuesbiologicalenergycandrawmoreandmoreattention.Anaerobicdigestiontechnologyasthemostprevalentmethodofsewagesludgestabilizationandrecyclationhasabroaddevelopmentprospect.ThedevelopmentofanaerobicreactorssuchasUASBEGSBICreactionmechanismoperatingrulesadvantagesanddisadvantagesaswellasapplicationstatusofdomesticandforeignscholarsstudyingonthemwerediscussed.Thedirectioninanaerobicreactorsdevelopmentwasintroduced.Moreovertheproblemsneededforfurtherstudywerepointedout.Keywordsanaerobicreactorsdevelopmenttypicalreactorsresearchprospects1990-。1953-。。11990-2003100m32003460m320111050m3。2。3、。。。Bryant4Zeikus5。。11881100。。1.118966。1904Imhoff7。19146。2050Schroepfer8。4513331.22060。1969Young239。1974LettingaUASB10。11。1.3。2080。22.1UpflowAnaerobicSludgeBlanketUASBUASB12。1972-1978LettingaUASB10。UASB、131。。。。。。。1UASBFig.1SchematicdiagramofUASBreactorShigeki14UASB1325℃HRT4.7h6CODCOD80%70%。15COD7.2kgCOD/m3·d80%CH46.2L/d。2.2expandedgranularsludgeblanketEGSBEGSBUASB。2080WageningenEGSB。COD16。EGSB2、、、17。。。2EGSBFig.2SchematicdiagramofEGSBreactorKato1830℃EGSBCOD100200mg/L12kgCOD/m3·dHRT4hCOD80%。19EGSB20℃、HRT18h184dEGSB10kgCOD/m3·dCOD85%1kgCOD0.58m3。2.3internalcyclicreactorICUASB2080PAQUES20。IC2UASB。、、213。。。。3420177。。。。。3ICFig.3SchematicdiagramofICreactorPengyiCui22IC。SCOD3500mg/L18kgCOD/m3·d68%SCOD6600mg/L16kgCOD/m3·d60%。23ICOLR。1.0m/hOLR2.5018.94kgCOD/m3·dCOD85%4.49L/L·d。COD60%81%。3。。12fluent。3。4。5。6。、。1.J.201024133-133.2.J.2007222174-176.3.—D.2007.4LafitteTSForsterCF.Dualanaerobicco-digestionofsewagesludgeandconfectionerywasteJ.BioresourceTechnology200071177-82.5.J.2008s1215-219.6.J.200324482-86.7HAANDELAVKATOMT.AnaerobicReactorDesignConceptsfortheTreatmentofDomesticWastewaterJ.ReviewsinEnvironmentalScienceandBio/Technology20065121-38.8SCHROEPFERGJANDERSONJJ.TheanaerobiccontactprocessasappliedtopackinghousewastesJ.Sewage&IndustrialWastes1955274460-486.9YOUNGJCMCCARTYPL.TheanaerobicfilterforwastetreatmentJ.Journal-WaterPollutionControlFederation1969415SupplR160+.10LETTINGAGHAANDELAC.AnaerobicdigestionforenergyproductionandenvironmentalprotectionJ.RenewableEnergySourcesforFuels&Electricity1993817-839.11.J.200422212-17.12.UASBJ.2008325655-660.13.UASBD.2008.14UEMURASHARADAH.TreatmentofsewagebyauasbreactorundermoderatetolowtemperatureconditionsJ.BioresourceTechnology2000723275-282.15.UASBJ.201483851-856.16.EGSBJ.200512330-32.17.EGSBD.2007.18KATOMTFIELDJALETTINGAG.TheanaerobictreatmentoflowstrengthwastewatersinuasbandegsbreactorsJ.WaterScience&Technology1997366375-382.19.EGSB20℃J.2008294990-995.20.icD.2005.21.ICJ.200022339-41.22CUIPYZHOUXFZHANGYL.ThefeasibilitystudyofcottonpulpwastewatertreatmentwithicanaerobicreactorJ.ProcediaEnvironmentalSciences2011111686-692.23LUOGLIJLIYetal.PerformancekineticsbehaviorsandmicrobialcommunityofinternalcirculationanaerobicreactortreatingwastewaterwithhighorganicloadingrateRoleofexternalhydrauliccirculationJ.BioresourceTechnology2016222470-477.
本文标题:高效厌氧反应器的研究进展杨闪
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